• Proceedings of the Membrane Society of Korea Conference
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• 1993.04a
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• pp.1-11
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• 1993

Cartridge filters are widely used in liquid-solid separation processes. To select a proper filter system for the requirements of a given application, a knowledge of filter efficiency and dirt capacity is required. The filter manufacturer needs to provide data which are based on test procedures simulating real parameters on a laboratory scale. There does not exist at present a standard for liquid filter testing (with the exception of the Multipass Test to ISO4752 for hydraulic filters). Users have to work with data based on different test procedures. This paper will discuss principles of filter testing, efficiency andd dirt capacity results as a function of test parameters, and data interpretion to provide a guideline for the end user.

• Proceedings of the Membrane Society of Korea Conference
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• 1995.03a
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• pp.69-83
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• 1995

지난 수십년산 부직포 산업에 대한 관심이 증대되고 있고, 정부차원에서 환경문제에 관심이 고조되면서 부직포를 이용한 FILTER의 수요는 꾸준히 늘고 있다. 특히 대구의 페놀사건 및 리우회담 개최등으로 환경문제에 전국민이 적극적으로 대응하고 관심의 영역이 급속히 넓어짐으로 인하여 공해방지용 각종 FILTER와 집진기용 FILTER의 수요가 상당히 증가하고 있는 실정이다. 또한 리우회담을 계기로 정부의 공해방지 및 환경에 대한 규제도 대폭 강화되었다. 이에 따라 기존의 직물을 소재로한 여과매체보다 형태의 안전성, 다양성, FILTERING 효과에서 앞서고 있는 부직포의 여과매체에 대한 관심이 점차 높아지고 있는 실정이다. 따라서 아직 개발하지 못한 부직포를 이용한 FILTER의 개발이 시급하고, 미개척 분야 에서의 부직포 사용을 위한 연구가 꾸준리 이루어져야 하겠다. 그리고 환경규제가 강화됨에 따른 고성능 여과포의 개발 또한 시급한 실정이다. 본장에서는 부직포를 이용한 여과매체, 즉 BAG FILTER의 제조 및 선정등에 대하여 간략하게 소개하고 추후 부직포 산업의 활성화에 미약하나마 보탬이 되길 바란다.

• KSBB Journal
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• v.6 no.2
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• pp.135-141
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• 1991

This study thus looks into two treatment processess : i) Anaerobic digester coupled with hollow fibre membrane unit. Treatment of starch waste with anaerobic digester-membrane system was studied. $0.17\m^2$ area of hollow fibre membrane unit of known pore size was immersed into laboratory-scale anaerobic digestion system. The pore size of membrane was varied from 0.03 to $\0.15mu$m. The hydraulic retention time of anaerobic digester was varied from 1.5 to 10 days. The effect of hydraulic retention time on treatment efficiency was significant while effect of membrane size was not significant. The gas production was about 0.74㎥/kg COD treated. The COD removal efficient was about 80-95% depending on the hydraulic retention time. ii ) Crossflow ultrafiltration as post treatment to anaerobic filter. The effluent from anaerobic filter, which had a total COD in the range of 4,500-5,200 mg/L was treated by crossflow ultrafiltration units. The study conducted with different membrane pore size indicated that membrace with 1,000,000 molecular weight cut-off size gave a higher COD removal efficiency in the range of 83-87% while giving a study flux of $120-130 L/\m^2$.h. A study was conducted to see the long term clogging effect of membrane also.

• Journal of Periodontal and Implant Science
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• v.23 no.3
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• pp.577-594
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• 1993

The ultimate goal of periodontal therapy is the regeneration of the periodontium that have been destroyed as a result of periodontal disease. This study were done in order to determine the healing status of periodontium under Polytetrafluoroethylene and millipore fillter combined with fibrin and the effect of the guided tissue regeneration procedures were performed as follows : 1) flap operation using PTFE membrane(control group) 2) flap operation using PTFE membrane which was fixed with fibrin(experimental group 1) 3) flap operation using millipore filter which was fixed with suture(experimental group II) 4) flap operation using millipore filter which was fixed with fibrin(experimental group II) After 1, 2, 4, 8, 12 weeks, dogs were sacrificed by perfusion technique and tissue block was excised including the tooth and prepared for light microscope with H-E & Masson’s trichrome staining. The result were as follows : In control and experimental group, there is no siginificant difference on epithelial cell down growth within 1st week, but more epithelial cell downgrowth in millipore or millipore combined with fibrin group. In this experiment, there were no significant difference in new cementum and alveolar bone formation whether PTFE membrane was fixed with suture or fibrin. In control and each experimental group, bone maturation appeared in 4 weeks, bone width increased bucco-lingually in control and experimental 1 group especially. Both control group and experimental group showed mild mew cementum formation on root surface and irregular arrangement of collagen fiber at 4 weeks, that showed obvious increased cementum formation at 8 weeks, and that was observed the functional arrangement of collagen fiber between new cementum and new alveolar bone at 12 weeks.

• Journal of Korean Society of Water and Wastewater
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• v.37 no.4
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• pp.187-202
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• 2023

This study focuses on the application of a new measurement method that quantifies the residual color of filtered water using a spectrocolorimeter after filtering the discolored substances. It was confirmed through the color and turbidity cross-test that the discolored substances cannot be measured effectively with the current legal color and turbidity test method. Therefore, the National Institute of Environmental Research's filter testing method, which involves filtering the sample through 0.45 ㎛ filter and visually inspecting the color, was improved. A membrane filter colorimetry (MFC) method was established by measuring the color difference (ΔE*ab(65)) of the filtered filter using a spectrophotometer and expressing it as filter color unit (FCU). Using the MFC method, the FCU for reference materials such as iron and manganese, as well as field samples, was measured. The results showed a high correlation with turbidity, and the color difference patterns varied depending on the type of reference materials and field samples. This indicates that the MFC method is an effective new measurement method of discolored tap water.

• Food Science and Preservation
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• v.10 no.4
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• pp.482-487
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• 2003

The filtration effects of glass membrane filters and hollow fiber membranes with different pore size to prevent the haze of a commercial foxtail millet Yakju were investigated. The most particles(haze precusors) present in the Yakju were removed by using 1.2 $\mu\textrm{m}$ glass membrane filter. In case of using 0.45$\mu\textrm{m}$ hollow fiber membrane system, the permeate flux on the Yakju filtration was calculated to 342.8 lmh. During the 3 month storage at 4$^{\circ}C$ and room temperature for each 48 hrs in turn, alittle fine haze was observed from the Yakju even if it was filtered by using 0.7 $\mu\textrm{m}$ glass membrane filter. Anything of haze was, however, observed from the Yakju filtered by using all of hollow fiber membranes. Therefore, the 0.45$\mu\textrm{m}$ hollow fiber membrane system was effective as a final filtration process of the Yakju.

• Proceedings of the Membrane Society of Korea Conference
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• 1997.10a
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• pp.107-108
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• 1997

1. 서론 : 분리막 시설의 전처리방법에는 Sand Filter, 유니필터 그리고 케트리지(5$\mu$m) 필터가 상용되어 왔다. 그러나 Sand Filter와 유니필터 등은 설치비용은 저렴하지만 처리수질이 5$\mu$m 케트리지 필터보다 떨어지므로 분리막시설의 전처리로 미흡하다. 통상적인 분리막 시설의 설계시에 사용되는 5$\mu$m 케트리지 필터는 역세가 불가능하므로 교체하지만 대규모의 수처리설비나, SS의 농도가 높은 경우에 있어서 분리막의 전처리시설로 적합치 않다. 한편 5$\mu$m 케트리지 필터는 대체하기 위한 정밀여과장치가 많이 개발되고 있으며 Z필터, BMF, Cross Filter 등이 그러한 여과장치들이다. 본 글에서 소개할 VPMF(Variable Pore Micro Filter, 가변세공 정밀여과장치)도 그러한 여과장치와 유사한 기능과 성능을 가진 정밀여과장치이다. 본 연구에서는 Caolin을 이용하여 50~100ppm 사이의 SS농도하에서 VPMF의 처리수질, 역세효율, SS포집능력 등을 평가해 볼 것이다.

• Proceedings of the Membrane Society of Korea Conference
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• 1993.10a
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• pp.40-41
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• 1993

생물 ㅏ반응기의 생산성을 높이기 위해서는 반응기내의 미생물 농도를 높이는 것이 필요하다. 미생물 농도를 높이기 위한 한 방법으로써 막을 이용한 미생물 재순환에 대한 많은 연구가 수행되어 왔다. 이러한 연구들은 발효조 밖에서 막을 이용하여 미생물을 분리하여 다시 발효조 내로 순환시키는 방법이 주를 이루어 왔으나 이들은 공정이 복잡하고 고분자 합성막을 이용한 경우 고온 멸균의 어려움이 있는등 산업화하는데 여러가지 문제점을 가지고 있었다.

• Proceedings of the Membrane Society of Korea Conference
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• 1991.04a
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• pp.19-22
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• 1991

생물 반응기내에 미생물 농도를 높이기 위한 한 방법으로써 막을 이용한 미생물 재순환에 대한 연구가 이루어져 왔다. 이러한 연구들은 발효조 밖에서 막을 이용하여 미생물을 분리하여 다시 발효조 내로 순환시키는 방법이 주를 이루었으나 이들은 공정이 복잡하고 고분자 합성막을 이용한 경우 고온 멸균의 어려움 등 산업화하는데 여러가지 문제점을 가지고 있었다.

• Journal of Korean Society of Water and Wastewater
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• v.12 no.1
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• pp.102-107
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• 1998

This study was conducted to investigate how the pore sizes of MF and UF membranes affected the removal efficiencies. The experimental results were compared with those obtained from the existing sand filter to select the optimum membrane. Turbidity of the raw water was adjusted to 10, 30, 50, 100, and 200NTU. The removal efficiencies of the turbidity and SS were nearly 100% for all membranes applied. Not membrane differences in the removal efficiencies of dissolved organics were also found. Thus, MF membrane with pore size $0.1{\mu}m$ was selected to obtain satisfactory removal efficiencies of turbidity and bacteria. Permeable flux was also considered. The $0.1{\mu}m$ MF membrane system was operated in the treatment plant to compare the results with those obtained from the existing sand filter. Turbidity, SS, $KMnO_4$ consumption, and number of coliform were chosen to be compared. Because there were not much differencies in the quality of the treated water, the existing coagulation-sedimentation-filtration process might be replaced and upgraded by simpler membrane process.